4.4 Article

Pretreatment of Mango (Mangifera indica L. Anacardiaceae) Seed Husk for Bioethanol Production by Dilute Acid Treatment and Enzymatic Hydrolysis

Journal

APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY
Volume 193, Issue 5, Pages 1338-1350

Publisher

SPRINGER
DOI: 10.1007/s12010-020-03387-7

Keywords

Bioethanol; Dilute acid treatment; Enzymatic hydrolysis; Lignocellulosic biomass; Mango seed husk; Pretreatment strategies

Funding

  1. Department of Science and Technology-Engineering Research and Development for Technology (ERDT) program

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This study addresses the challenges faced by the Biofuels Act of 2007 in the Philippines by exploring the potential of mango seed husk (MSH) as a feedstock for bioethanol production. Results show that a combined process strategy of dilute acid pretreatment followed by enzymatic hydrolysis can increase the concentration and yield of sugars in the hydrolysates, which is advantageous for bioethanol production.
One of the targets of the Sustainable Development Goals is clean and affordable energy. This is also the aim of the Biofuels Act of 2007 in the Philippines. However, this law is confronted with challenges such as the limitation of lignocellulosic feedstock, specifically available for bioethanol production. The present study sought to address the issue by exploring the potential of mango seed husk (MSH), a by-product of the mango industry, in bioethanol production. MSH is considered a waste material and its utilization also permit value-addition as this can serve as an alternative and affordable source of feedstock in energy production. Two pretreatment strategies are employed to exploit the cellulose and hemicellulose content of MSH, namely, dilute acid treatment and enzymatic hydrolysis. Results show that the %H2SO4 resulting in the highest glucose concentration and yield is 4%v/vat 95 degrees C hydrolysis temperature, 1:10 (w/v) solid-to-solvent ratio, and 60-min hydrolysis time. For enzymatic hydrolysis using a commercial enzyme preparation, the reaction time up to 72 h did not affect glucose concentration and yield at the following conditions: 50 degrees C hydrolysis temperature, 150 rpm, pH 5.0, 10% solids loading, and 4% enzyme loading. This could be attributed to the lignin and non-structural compounds present in MSHs. However, a combined process strategy of dilute acid pretreatment followed by enzymatic hydrolysis in the pretreatment of MSH contributes to an increased concentration and yield of sugars in the hydrolysates, which is advantageous for bioethanol production.

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